Metal catalysts impregnated on porous media for aqueous phenol decomposition within three-phase fluidized-bed reactor

被引:11
|
作者
Mungmart, M. [1 ]
Kijsirichareonchai, U. [1 ]
Tonanon, N. [1 ]
Prechanont, S. [1 ]
Panpranot, J. [1 ]
Yamamoto, T. [3 ]
Eiadua, A. [3 ]
Sano, N. [4 ]
Tanthapanichakoon, W. [1 ]
Charinpanitkul, T. [1 ,2 ]
机构
[1] Chulalongkorn Univ, Ctr Excellence Particle Technol, Fac Engn, Bangkok 10330, Thailand
[2] Chulalongkorn Univ, Energy Res Inst, Bangkok 10330, Thailand
[3] Natl Inst Adv Ind Sci & Technol, Tsukuba, Ibaraki 3058565, Japan
[4] Kyoto Univ, Dept Chem Engn, Kyoto 6712201, Japan
关键词
Phenol; Metal catalyst; Porous media; Three-phase fluidized bed; ACTIVATED CARBON; WATER-TREATMENT; OXIDATION; OZONE;
D O I
10.1016/j.jhazmat.2010.09.061
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Performance of metal catalysts to decompose aqueous phenol was experimentally investigated. Comparison of the phenol decomposition rates within three-phase fluidized-bed reactors utilizing only O-3. TiO2 deposited on silica beads, metal catalyst (Ni or Co) impregnated on mesoporous carbon beads, or O-3 in combination with each catalyst was thoroughly examined. It was found that the use of Co catalyst with the presence of O-3 led to the best removal condition which aqueous phenol was completely decomposed within 10 min (k = 0.1944 min(-1)). In contrast, the use of TiO2 without O-3 resulted in the worst decomposition of phenol (k = 0.0066 min(-1)). Some intermediate products, such as hydroquinone and catechol, were also detected but their final concentrations were negligibly low. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:606 / 612
页数:7
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